Rapid Sand Filters
Rapid sand Water filter does not use biological filtration and depends primarily on mechanical mechanical straining, straining, sedimentation, sedimentation, impaction, impaction, interceptio interception, n, adhesion adhesion and physical physical adsorption. In Rapid sand water filter the complete filtration cycle (filtration and back washing) occurs sequentially. Filters that must be taken off-line periodically to back wash a re classified operationally as semi-continuous. Water Treatment Filters in which filtration and backwash operations occur simultaneously are classified as continuous. Types of Rapid Sand Filter
There are a number of different types of Rapid of Rapid sand filters depending upon bed depth (e.g., shallow, conventional and deep bed) and the type of filtering medium used (mono-, dual-, and multimedia). A further classification can be made based on the driving force as gravity or pressure filters. Typically sand is used as the filtering material in single medium filters. Dualmedium filters usually consist of a layer of anthracite over a layer of sand. Multimedia filters typically consist of a layer of anthracite over a layer of sand over a layer of garnet. The principal filtration methods now used with reference to the rate of flow through gravity filters may be classified as • • •
constant-rate of filtration with fixed head, constant -rate filtration with variable head, and variable- declining-rate filtration.
Constant-rate Filtration with fixed head
In constant-rate filtration with fixed head, the flow through the filter is maintained at a constant rate. They are either in-fluent controlled or effluent controlled. Pumps or weirs are used for in-fluent in-fluent control whereas an effluent effluent modulating modulating valve that can be operated manually or mechanically is used for effluent control. Constant-rate Filtration with variable head
In constant-rate variable filtration head, the flow through the filter is maintained at a constant rate. Pumps or weirs are used for in-fluent control. When the head or effluent turbidity reaches a preset value, the filter is back-washed. Declining-rate filtration with fixed or variable head
In declining-rate filtration, the rate of flow through the filter is allowed to decline as the rate of head loss builds up with time. Declining-rate filtration systems are either in-fluent controlled or effluent controlled. In the effluent controlled type of filters, the filter effluent lines are connected to a common header. A fixed orifice is built into the effluent piping for each filter so that no filter after washing will take an undue share of the flow. The filtered water header pressure may be regulated by a throttle valve which discharges to filtered water reservoir. Costly rate controllers are replaced with fixed orifices and therefore, would make the units economical particularly in large water works involving batteries of filters. For equal duration of filter runs the total output per day from a declining rate filter is higher than that in the conventional filters. In group of filters operating at an average rate of 10 m3/m2/hr, the fixed orifice will be so designed that a recently cleaned filter will begin operation at 15 m3/ m2/hr while the filter next in line for cleaning will have slowed down to about 5 m3/m2/hr. Usually the depths of filter boxes for declining rate filters are more than those for the conventional ones. These would permit longer filter runs and consequent reduced wash water requirements. The filter beds are operated by scheduled cleaning in such a way that each of beds will be in different stage of filter cycle producing the required average flow. When the rate of flow is reduced to the minimum design rate, the filter is removed from service and backwashed. In an inlet-controlled filter, the rate of flow is controlled proportional to the rate of filtration with float control arrangement to the inlet valve. Inlet control reduces the amount of work which has to be done on the filter to just clean it. Components of Rapid sand filter
The major parts of a gravity rapid sand filter are: • • • •
Filter tank or filter box, Filter media, Gravel support, Under drain system, and
Wash water troughs
The Above Figure shows a typical rapid sand filter with components. The filter is contained within a filter box, usually made of concrete. Inside the filter box are layers of filter media and gravel. Below the gravel, a network of pipes makes up the under-drain system which collects the filtered water and evenly distributes the backwash water. Washwater troughs help distribute the in-fluent water and are also used in collecting the dirty washed water during backwashing.
In addition to the components mentioned above, most rapid sand filters contain a flow controller, or filter control system, which regulates flow rates of water through the filter. Other parts, such as valves, a loss of head gauge, surface washers, and a backwash pump, are used while cleaning the filter. Operation of a Rapid sand filter during filtration is similar to operation of a Slow sand filter. The influent water flows down through the sand and support gravel and is collected by the underdrain system is shown in the above Figure. However, the influent water in a rapid sand filter is already relatively clear due to coagulation, flocculation and clarification, so RSFs operate much more quickly than SSFs. The rate of filtration varies from 80 to 120 Lpm/ m2 (4800 to 7200 Lph/ m2) of filter bed area or 4.8 to 7.2 m/ h. The average rate of filtration for design purpose may b e assumed as 100 Lpm/ m20f filter area or (6m/h). Filter Tank
The filter tank is generally constructed of concrete and is most often rectangular. Filters in large plants are usually constructed next to each other in a row, allowing the piping from the clarifier basins to feed the filters from a central pipe gallery or from a inlet channel. The sizes of the filters vary according to the quantity to be treated. The number of filters is selected to minimize the effect of removing the filter from service for washing on remaining filters. The larger the number, therefore, the better it is, for the proper operation. Ideally it should be possible to take three filters out of service simultaneously (one draining down, one washing and one for maintenance). A minimum of four filters is desirable, although two to three filters may be u sed for small plants. Filter bed sizes vary from 25 to 100 m2 with lengths in the range of 4 to12 m and widths in the range of2.5 to 8 m and length to breadth ratio of1.25 to 1.33. The wash water collection channel is located on one side along the length of the filter. Filter beds of twice this size can be constructed as two identical beds separated by the wash water collection cham1el, thus limiting the length of travel of feed water to 5 m. A minimum overall depth of 2.6 m including a free board of 0.5 m is adopted. Fig shows the cut section of RSF box showing the under drainage system, gravel, sand media and wash water gu tters. The filter media is the important component of the filter which actually removes the particles from the water being treated. Filter media is most commonly sand, though other types of media can be used, usually in combination with sand. The sand used in rapid sand filters is coarser than the sand used in slow sand filters. This larger sand has larger pores which do not fill as quickly with particles removed from the water. Coarse sand also costs less and is more readily available than the finer sand used in slow sand filtration. The filter sand used in rapid sand filters is prepared from stock sand specifically for the purpose. Most rapid sand filters contain 60 to 75 cm thickness of sand, but some newer filters are deeper. The sand used as filter media in RSF is generally of effective size of 0.4 to 0.7 mm and uniformity coefficient of 1.3 to 1.7. The standing water depth over filter varies between 1.0 and 2.0 m.
Graded Gravel
The filter gravel at the bottom of the filter bed is not part of the filter media and it is merely providing a support for media above the underdrains and allowing an even distribution of flow of water across the filter bed during filtering and backwashing. The gravel also prevents the filter sand from being lost during the operation. The filter gravel is usually graded of size from 2.5 to 50 mm (largest size being at the bottom) in four to five layers to total thickness of 45 to 50 cm, depending on the type of under drain system used. In case the under drainage system with pourous bottom or false floor no gravel base is required. The filter gravel shall be classified by sieves into four or more size grades, sieves being placed with the coarsest on top and the finest at the bottom. Under-drainage System for Rapid Sand Filter s
The under-drainage system of the filter is intended to collect the filtered water and to distribute the wash water during backwashing in such a fashion that all portions of the bed may perform nearly the same amount of work and when washed receive nearly the same amount of cleaning. Since the rate of wash water flow is several times higher than the rate of filtration, the former is the governing factor in the hydraulic design of filters and under drainage system, which are cleaned by backwashing . The under-drainage system can be one of the following types, connected to main drain: • • •
Pipe laterals False floor Porous plates or strainer nozzles
The most common type of under-drain is a central manifold with laterals either perforated on the bottom or having umbrella type strainers on top. Other types such as wheeler bottom, a false bottom with strainers spaced at regular intervals or a porous plate floor supported on concrete pillars are all satisfactory when properly designed and constructed. Wash-water Troughs
Wash-water troughs placed above the filter media collect the backwash water and carry it to the drain system. Proper placement of these troughs is very important to ensure that the filter media is not carried into the troughs during the backwash operation and removed from the filter. The upper edge of the washwater trough should be placed sufficiently nearer to the surface of sand so that a large quantity of dirty water is not left above the filter sand after completion of washing. At the same time, the top of the wash-water trough should be placed sufficiently high above the surface of the sand so that the sand will not be washed into the gutter. Width of the filter bed must be equally divided by the troughs so that each trough covers an equal area of the filter. Maximum clear spacing between the troughs may be 180 cm. The horizontal travel of wash-water to trough should not be more than 90 cm. All the
wash water troughs must be installed at the same elevation so that they remove the backwashed water evenly from the filter so that an even head is maintained across the entire filter. The troughs may be made with the same cross-section throughout its length or it might be constructed with varying cross-section increasing in size towards the outlet end. The bottom of the troughs should clear the top of the expanded sand by 50 mm or more. These wash water troughs are constructed in concrete, plastic, fiberglass, or other corrosion-resistant materials. The troughs are designed as free falling weirs. Backwashing
Proper backwashing for cleaning the filter is a very important step in the operation of a filter. If the filter is not backwashed periodically, it will eventually develop additional operational problems. If a filter is to operate efficiently during a filter run it must be cleaned regularly at every 24 to 48 hours. Treated water from storage is used for the backwashing. This treated water is generally taken from elevated storage tanks or pumped in directly from the clear water drain by passing in the reverse direction from under drains to the media. The below Figure shows the flow pattern during the backwashing. During filtration, the grains of filter media become coated with the floes, which plug the voids between the filter grains, making the filter difficult to clean. Backwash should, therefore, be arranged at such a pressure that sand bed should expand to about 130 to 150% of its undisturbed volume so as to dislodge the deposited floes from the filter media during the backwash. Washing causes the sand grains to impinge on one another and thus dislodging adhering floc and, the rising wash water carries the material and discharge into the gutters. The backwash flow rate has to be great enough to expand and agitate the filter media and suspend the floes in the water for removal. On the other hand an unduly high rate of flow will cause more expansion than needed, so that the sand grains will be separated further and scrubbing action will be decreased and the media will be washed from the filter into the troughs and out of the filter. A normal backwash rate is 600 Lpm/ m2 of filter surface area without any other agitation. The pressure of the wash water to be applied is about 5 m head of water as measured in under drains. Backwashing normally takes about 10 minutes, though the time varies depending on the length of the filter run and the quantity of material to be removed. Filters should be backwashed until the backwash water is clean. For high rate back wash, the pressure in the under drainage system should be 6 to 8 m with wash water requirement being 650 to 850 Lpm/ m2 of filter (40 – 50 m/hr) for a duration of 6 to 10 minutes. Air Wash System
In most cases the filter backwash rate will not be sufficient to break up the mass on the top of the filter. During filter backwash, the media expands upwards and around the washing arms only. If air is forced through the under-drains until the sand is thoroughly agitated, for a period of about five minutes the expansion of sand media and complete removal of the floes could be achieved. In the air wash system, compressed air is used to secure effective scrubbing action with a sma:ll~r volume of wash water. The air may be
forced through the under drains before the wash-water is introduced or through a separate piping system placed between the gravel and the sand layer. Though the former results in better washing, the gravel is likely to be disturbed. The cleaning of filter with air agitation followed by backwash is a very efficient method but requires the installation of a large air blower to produce the air. The normal design of backwashing employing conjunctive air and water wash, air will be applied at 700 to 850 Lpm/ m2 of filter area (45 – 50 m/hr) and water at 200 to 250 Lpm/ m2 of filter area (1215 m/hr). Surface Washing
The upper layer of the filter bed becomes the dirtiest and any inadequate washing will lead to the formation of mud balls, cracks and clogged apots in the filters. These troubles are overcome by adequate surface wash which can be accomplished by stirring the expanded filter bed mechanically with jet of water directed into the suspended sand. Surface washers spray water over the sand at the top of the filter breaking down mud balls.The below Figure shows the surface wash arrangements.
